AU701569B2 - Method for producing consumer milk with good keeping qualities - Google Patents
Method for producing consumer milk with good keeping qualities Download PDFInfo
- Publication number
- AU701569B2 AU701569B2 AU34012/95A AU3401295A AU701569B2 AU 701569 B2 AU701569 B2 AU 701569B2 AU 34012/95 A AU34012/95 A AU 34012/95A AU 3401295 A AU3401295 A AU 3401295A AU 701569 B2 AU701569 B2 AU 701569B2
- Authority
- AU
- Australia
- Prior art keywords
- flow
- milk
- cream
- skim milk
- high temperature
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; PREPARATION THEREOF
- A23C9/00—Milk preparations; Milk powder or milk powder preparations
- A23C9/14—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment
- A23C9/142—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment by dialysis, reverse osmosis or ultrafiltration
- A23C9/1422—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment by dialysis, reverse osmosis or ultrafiltration by ultrafiltration, microfiltration or diafiltration of milk, e.g. for separating protein and lactose; Treatment of the UF permeate
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23B—PRESERVATION OF FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES; CHEMICAL RIPENING OF FRUIT OR VEGETABLES
- A23B11/00—Preservation of milk or dairy products
- A23B11/10—Preservation of milk or milk preparations
- A23B11/12—Preservation of milk or milk preparations by heating
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; PREPARATION THEREOF
- A23C9/00—Milk preparations; Milk powder or milk powder preparations
- A23C9/14—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; PREPARATION THEREOF
- A23C2210/00—Physical treatment of dairy products
- A23C2210/20—Treatment using membranes, including sterile filtration
- A23C2210/208—Removal of bacteria by membrane filtration; Sterile filtration of milk products
Landscapes
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Water Supply & Treatment (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Dairy Products (AREA)
- Seeds, Soups, And Other Foods (AREA)
- Edible Oils And Fats (AREA)
Abstract
PCT No. PCT/SE95/00864 Sec. 371 Date Jan. 16, 1998 Sec. 102(e) Date Jan. 16, 1998 PCT Filed Jul. 17, 1995 PCT Pub. No. WO96/36238 PCT Pub. Date Nov. 21, 1996A method for continuous production of consumer milk with a variable fat content including microfiltration of a flow of skim milk. From the microfilter there is obtained a retentate flow and a permeate flow. The permeate flow of skim milk is subjected to a heat treatment and is then mixed with a partial flow of high temperature treated cream product in a desired amount. From this, there is obtained consumer milk with a good keeping quality.
Description
WO 96/36238 PCT/SE95/00864 1 Method for producing consumer milk with good keeping qualities The present invention relates to a method for producing consumer milk with good keeping qualities.
In order to secure that milk that is delivered to the consumers does not contain pathogenic microorganisms the milk is heat treated prior to the packaging. This heat treatment may be carried through at different time/temperature combinations. Usual standards within this field are low pasteurization, high pasteurization and ultra pasteurization. Depending on the legislation in different countries the pasteurizing processes are different. As example of different processes there may be mentioned low pasteurization where the milk is heated to a temperature of 63-65 0 C and is kept at this temperature during 30 minutes or to 72-75C with a holding time of 12-40 seconds. When high pasteurizing the treatment may comprise heating to 100 0 C during 10-20 seconds and at ultra pasteurization 110- 125 0 C for 0.5-4 seconds.
A more forceful heat treatment gives a more complete killing of both pathogenic as other microorganisms present in the milk. The stronger the heat treatment the more pronounced is the effect on the chemical constituents, proteins, enzymes and vitamines in the milk which effect may be sensed as an impairment of the taste.
The shelf life of the packaged milk depends of course also on the treatment after the pasteurization step. It is extremely important to hinder reinfection during the process steps prior to the packaging in order to obtain good keeping qualities.
WO 96/36238 PCT/SE95/0064 2 In order to obtain a milk product with a good keeping quality and a good taste one balances between the desire to achieve a product with as good bacteriological quality as possible, which product at the same time has not been effected negatively by the necessary heat treatment.
One way of obtaining a milk product with an extended shelf life is described in SE 451 791. According to this patent milk is divided into a cream and a skim milk fraction by means of centrifugal separation. The skim milk fraction is led to a microfilter and is divided into a permeate with a low bacteria content and a concentrate with a higher fat content than the permeate in the microfilter. The cream fraction and the concentrate are sterilized and remixed in desired proportions with the permeate after which the mixture passes a final heat treatment. The milk obtained according to the patent which is bacteria-poor may for example be used for producing cheese or be sold as consumer milk with extended shell life.
According to the invention there is now proposed a method of continuously producing a consumer milk with good keeping qualities where no part of the milk flow has been subjected to more than one heat treatment. In many countries the legislation forbids more than one heat treatment. According to the method of the invention a flow of skim milk is brought to pass a microfilter from which there is obtained a retentate flow and a permeate flow. The obtained permeate flow is subjected to a heat treatment and is then remixed with a partial flow of high temperature treated cream product in a desired amount in order to give a consumer milk with a long shelf life.
WO 96/36238 PCT/SE95/0064 3 In the patent application the expression cream product is used. Some twenty years ago there was on the market mainly two different kinds of cream, namely whipping cream with a fat content of 35-40 and thin cream with a fat content of 12-15 When separating whole milk in a centrifugal separator there is obtained a cream fraction with a fat content of about 40 and a skim-milk fraction with a fat content of 0.05 With the present-day supply of different types of cream with fat contents from 6 to 60 the word cream is no longer unambiguous and in the present patent application the expression cream product is used to cover the different variations in fat content.
With high temperature treatment one usually refers to a heating to a temperature above 110 0 C during 2-10 seconds.
The microfiltration of the skim milk may be carried through in direct connection to the skimming, i.e. the separation of cream from the skim milk in a centrifugal separator. In such a case a part of the flow of cream which has left the centrifugal separator is used. This cream has a fat content of 40 However, it is also possible to use a cream product with a lower fat content which after sterilization is mixed with the microfiltrated skim milk to give the desired fat content in the consumer milk. Such a cream product may be produced from the cream which is obtained during the skimming, the centrifugal separation, by mixing skim milk in the cream either in direct connection to the separation or in a later step.
If so is desired the cream product may be mixed with a portion of skim milk or microfiltrated skim milk prior to WO 96/36238 PCT/SE95/00864 4 the sterilization which portion is taken from the main flow of microfiltrated skim milk prior to the heat treatment step.
The permeate flow of skim milk may be subjected to a heat treatment to a temperature of 50-72 0 C during up to seconds. Such a treatment with an undefined combination of temperature and time is of value when a minimal influence on the constituents of the milk is desired. Such a low temperature treatment may be followed by a pasteurization of the milk at some later step.
Preferably the permeate flow of skim milk is subjected to any appropriate pasteurization process. Such pasteurization may involve heating the permeate flow to 70-85C for 2-30 seconds or high pasteurization, i.e. heating to 85-140°C for 1-10 seconds. The desired degree of pasteurization is chosen depending on for example the legislation in different countries or on the purpose of the heat treatment i.e. to achieve a milk with as long a shelf life as possible or a milk with both good taste and good shelf life. The quality of the initial whole milk may of course also influence the choice of pasteurization level.
According to the invention the mixture of the portion of microfiltrated skim milk and cream product may suitably be brought to pass a homogenizer in order to achieve a desired amount of finely divided fat spheres.
The fat content of said mixture of cream product and skim milk is suitably below 25 during the homogenization.
The retentate flow from the microfilter may if so is desired be mixed with the partial flow of cream product and WO 96/36238 PCT/SE95/00864 WO 96/36238 PTS9106 5 sterilized together with the same. The retentate flow may alternatively be taken care of in some other way.
The method according to the invention is described further with reference to the attached drawing which shows a flow chart of an example of a method of producing pasteurized consumer milk. As is seen from this whole milk is heated prior to the centrifugal separation. A suitable temperature may be 55°C. The whole milk is divided into a flow of cream with a fat content of 40 and a flow of skim milk with a fat content of 0.05 If so is desired a part of the skim milk may be returned immediately to the cream in order to give a cream product with a lower fat content. The obtained skim milk is led to a microfilter with a membrane with a pore size of 0.05-2.0 p, suitably 1.4 p and is divided into a bacteria poor permeate stream and a bacteria rich retentate stream. A part of the cream flow from the centrifugal separator is taken away and passes a high temperature treatment 120'C, 2 seconds. The retentate flow from the microfilter may if so is desired be mixed with the flow of cream prior to the high temperature treatment. Of 100 1 whole milk the retentate flow constitutes 4,5 1 according to this example. Alternatively, a partial flow of microfiltrated skim milk may be led away from the permeate flow and be mixed with cream prior to the high temperature treatment. The bacteria poor permeate flow is pasteurized, for example at 72 0 C with a holding time of 15 seconds. A portion of the permeate flow which has passed the pasteurization is remixed with high temperature treated cream product and is led to a homogenizer. The amount of pasteurized, microfiltrated skim milk which is mixed with the cream product may be 0-35 1 (counted on the initial amount 100 After homogenization of the cream-skim milk mixture said mixture is remixed with the pasteurized WO 96/36238 PCT/SE95100864 6 permeate flow of skim milk. After cooling the milk is packaged.
The milk which has been obtained according to the method of the invention has a good taste since no portion of the same has passed more than one heat treatment. The bacteria content is compared to milk which only has been pasteurized, more than 100 times lower, which means a considerably extended shelf life.
WO 96/36238 PCTISE95/00864 7 Whole milk Preheating Separation Skim milk Cream Microfiltration Permeate Retentate Pasteurization High Temperature treatment Homogenization Cooling Storage/Packaging SUBSTITUTE SHEET
Claims (5)
1. Method for production of consumer milk with extended shelf-life, comprising the steps of separating whole milk in a fraction of cream and a fraction of skim milk, bringing a flow of said fraction of skim milk to pass through a microfilter from which is obtained a flow of retentate and a flow of permeate, for purpose of sterilising treating a flow of said cream fraction at a high temperature, and remixing said high temperature-treated flow of cream with said permeate flow to forming said consumer milk, characterized in that said permeate flow is pasteurized prior to remixing with the high temperature-treated cream flow, whereby the flow of separated cream as well as said permeate flow are subjected to not more than one heat treatment, i e high temperature treatment and pasteurizing, respectively.
2. Method according to claim 1, characterized in that the cream product prior to the high temperature treatment is mixed With a portion of not yet heat treated microfiltrated skim milk.
3. Method according to claim 1 or 2, characterized in that the mixture of cream product and skim milk is brought to pass a homogenizer.
4. Method according to claim 3, characterized in that the fat content of the cream-skim milk mixture during the homogenization is below 18%.
5. Method according to claim 1 or 2, characterized in that the retentate flow from the microfilter is mixed with the partial flow of cream product and passes the high temperature treatment together with the same. AMENDED SHEET
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SE9501822A SE506683C2 (en) | 1995-05-17 | 1995-05-17 | Way to make consumable milk with long shelf life |
| SE9501822-2 | 1995-05-17 | ||
| PCT/SE1995/000864 WO1996036238A1 (en) | 1995-05-17 | 1995-07-17 | Method for producing consumer milk with good keeping qualities |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AU79479/98A Addition AU738775C (en) | 1997-06-19 | 1998-06-15 | A method for the production of sterile skimmed milk |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| AU3401295A AU3401295A (en) | 1996-11-29 |
| AU701569B2 true AU701569B2 (en) | 1999-02-04 |
Family
ID=20398336
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AU34012/95A Expired AU701569B2 (en) | 1995-05-17 | 1995-07-17 | Method for producing consumer milk with good keeping qualities |
Country Status (27)
| Country | Link |
|---|---|
| US (1) | US5935632A (en) |
| EP (1) | EP0828429B1 (en) |
| JP (1) | JP3667343B2 (en) |
| KR (1) | KR100384657B1 (en) |
| CN (1) | CN1061516C (en) |
| AT (1) | ATE226020T1 (en) |
| AU (1) | AU701569B2 (en) |
| BR (1) | BR9510588A (en) |
| CA (1) | CA2221164C (en) |
| CZ (1) | CZ291739B6 (en) |
| DE (1) | DE69528605T2 (en) |
| DK (1) | DK0828429T3 (en) |
| EE (1) | EE03300B1 (en) |
| ES (1) | ES2186728T3 (en) |
| FI (1) | FI119904B (en) |
| HU (1) | HU224133B1 (en) |
| LT (1) | LT4376B (en) |
| LV (1) | LV11978B (en) |
| MX (1) | MX9708723A (en) |
| NZ (1) | NZ292283A (en) |
| PL (1) | PL323346A1 (en) |
| PT (1) | PT828429E (en) |
| RU (1) | RU2143814C1 (en) |
| SE (1) | SE506683C2 (en) |
| SI (1) | SI9520155A (en) |
| UA (1) | UA52601C2 (en) |
| WO (1) | WO1996036238A1 (en) |
Families Citing this family (42)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SE506854C2 (en) * | 1996-06-27 | 1998-02-16 | Tetra Laval Holdings & Finance | Ways of producing aseptic consumption milk |
| US6652900B2 (en) | 1997-03-14 | 2003-11-25 | Tetra Laval Holdings & Finance S.A. | Method and plant for producing a sterile milk product |
| US6326044B1 (en) | 1997-06-19 | 2001-12-04 | Tetra Laval Holdings & Finance S.A. | Filter apparatus and method for the production of sterile skimmed milk |
| SE519853E (en) * | 1997-06-19 | 2005-03-29 | Tetra Laval Holdings & Finance | Method of making sterile skim milk |
| US6372276B1 (en) | 1997-03-14 | 2002-04-16 | Tetra Laval Holdings & Finance S.A. | Method for producing sterile, stable milk |
| US6916499B1 (en) * | 1999-10-18 | 2005-07-12 | Land O'lakes, Inc. | Method of forming a light butter |
| US6737096B2 (en) | 2000-03-29 | 2004-05-18 | Tetra Laval Holdings & Finance S.A. | Method and apparatus for producing a sterile milk product |
| AU4321202A (en) | 2000-11-13 | 2002-06-24 | Tetra Laval Holdings & Finance | Sterile, stable milk and method for the production thereof |
| DE60129165D1 (en) | 2001-02-15 | 2007-08-09 | Niro Atomizer As | METHOD AND APPARATUS FOR THE PRODUCTION OF A MILK OR DAIRY PRODUCT WITH REDUCED SPORES AND BACTERIA CONTENT |
| NZ511095A (en) * | 2001-04-12 | 2003-06-30 | New Zealand Dairy Board | Subjecting a milk protein concentrate to cation exchange depleting the calcium content to produce a gel |
| RU2194415C1 (en) * | 2001-07-04 | 2002-12-20 | Общество с ограниченной ответственностью "Учебно-научно-производственная фирма "Липиды" | Method of preparing dietetic milk |
| ITVI20020166A1 (en) * | 2002-07-24 | 2004-01-26 | Cartigliano Off Spa | METHOD AND PLANT FOR THE CONDITIONING OF BIOLOGICAL LIQUIDS, PARTICULARLY MILK AND ITS DERIVATIVES |
| US20070166447A1 (en) * | 2002-08-27 | 2007-07-19 | Select Milk Producers, Inc. | Dairy compositions and method of making |
| RU2280395C2 (en) * | 2003-04-18 | 2006-07-27 | Олег Николаевич Дарашкевич | Method of sterilizing liquids |
| US20040226888A1 (en) * | 2003-05-14 | 2004-11-18 | Chandarana Dilip I. | Two stage sterilization of fluids that naturally support microbiological growth |
| ITPR20030047A1 (en) * | 2003-06-19 | 2004-12-20 | Parmengineering S R L | MILK TREATMENT PROCEDURE. |
| DE102005007941B4 (en) * | 2005-02-22 | 2008-01-31 | Martin Burger | Commissioning procedure of a milk sterilization plant and milk sterilization plant |
| WO2007035870A2 (en) | 2005-09-20 | 2007-03-29 | Prolacta Bioscience, Inc. | A method for testing milk |
| US20080160134A1 (en) * | 2006-12-27 | 2008-07-03 | Jamie Allen Hestekin | Method Of Producing Concentrated Liquid Dairy Products |
| US8110235B2 (en) * | 2008-05-06 | 2012-02-07 | Alliance Enterprises Of S.E. Wisconsin, Llc | Methods for reducing cholesterol in a milk product |
| US8092852B2 (en) * | 2008-05-15 | 2012-01-10 | I. Edward Salinas | Systems and methods for producing reduced cholesterol dairy products |
| US9055752B2 (en) * | 2008-11-06 | 2015-06-16 | Intercontinental Great Brands Llc | Shelf-stable concentrated dairy liquids and methods of forming thereof |
| JP5268817B2 (en) * | 2009-07-28 | 2013-08-21 | 森永乳業株式会社 | Process for producing processed milk or milk beverage |
| US20120183658A1 (en) * | 2009-09-16 | 2012-07-19 | Gea Mechanical Equipment Gmbh | Method for producing fresh milk having a longer shelf life |
| DE102010025664A1 (en) * | 2010-06-30 | 2012-01-05 | Unternehmensgruppe Theo Müller GmbH & Co. KG | Producing long-life milk, comprises separation, through which raw milk is separated into cream part and skimmed milk part, subjecting to mechanical treatment for separating microorganisms and/or their spores, and heating |
| UA112972C2 (en) | 2010-09-08 | 2016-11-25 | Інтерконтінентал Грейт Брендс ЛЛС | LIQUID DAIRY CONCENTRATE WITH A HIGH CONTENT OF DRY SUBSTANCES |
| KR101526132B1 (en) | 2011-08-15 | 2015-06-04 | 에픽 리서치 앤드 다이어그노스틱스 인코포레이티드 | Localized physiologic status from luminosity around fingertip or toe |
| RU2582258C2 (en) * | 2011-11-07 | 2016-04-20 | Тетра Лаваль Холдингз Энд Файнэнс С.А. | Method of production and device for production of initial milk material for skim milk |
| EP2777389B1 (en) * | 2011-11-07 | 2016-10-05 | Tetra Laval Holdings & Finance S.A. | Method for producing and device for producing cheese starting material milk |
| DK2661967T3 (en) * | 2012-05-11 | 2017-10-23 | Dmk Deutsches Milchkontor Gmbh | Process for making cheese milk |
| EP2661968B1 (en) * | 2012-05-11 | 2018-03-21 | DMK Deutsches Milchkontor GmbH | Process for making cheese dairy milk (II) |
| EP2679098B1 (en) * | 2012-06-26 | 2017-08-09 | DMK Deutsches Milchkontor GmbH | Milk powder having a high whey protein index |
| JP6199989B2 (en) * | 2013-12-03 | 2017-09-20 | キリン株式会社 | Reduced milk with good taste, flavor and emulsion stability, and production method thereof |
| GB2535538A (en) * | 2015-02-23 | 2016-08-24 | Arla Foods Ltd | Composition and process |
| EP3254566B1 (en) | 2016-06-08 | 2018-12-19 | DMK Deutsches Milchkontor GmbH | Process for making uht-milk with improved taste |
| EP3300606A1 (en) * | 2016-09-28 | 2018-04-04 | DMK Deutsches Milchkontor GmbH | Foamable milk composition |
| KR102697131B1 (en) * | 2016-10-04 | 2024-08-21 | 아이엠비 인코포레이티드 | Method and system for producing sterilized human milk products |
| BR112020010904B1 (en) * | 2017-12-22 | 2021-06-15 | Tetra Laval Holdings & Finance S.A. | METHOD AND SYSTEM FOR PRODUCING A FIRST DAIRY PRODUCT WITH A FIRST FAT CONTENT AND A SECOND DAIRY PRODUCT WITH A SECOND FAT CONTENT |
| KR102093020B1 (en) * | 2018-05-04 | 2020-04-23 | 남양유업 주식회사 | Method for manufacturing milk with high protein and calcium contents and low fat and cholesterol by only 100% pure milk |
| EP3639671A1 (en) * | 2018-10-17 | 2020-04-22 | Tetra Laval Holdings & Finance S.A. | Production of yoghurt milk and yoghurt |
| CN115191486A (en) * | 2021-04-14 | 2022-10-18 | 内蒙古伊利实业集团股份有限公司 | Method for improving stability of liquid goat milk and prepared liquid goat milk |
| CN117546913A (en) * | 2023-11-06 | 2024-02-13 | 皇氏赛尔生物科技(广西)有限公司 | Processing method of buffalo milk with high flavor reduction degree based on centrifugal separation technology |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3233964A (en) * | 1954-02-12 | 1966-02-08 | Purac Ab | Means for sterilizing liquid |
| CH573716A5 (en) * | 1973-12-21 | 1976-03-31 | Tetra Pak Dev | |
| SE429092B (en) * | 1980-10-30 | 1983-08-15 | Tetra Pak Dev | WAY TO PREPARE AND PACKAGE FOOD PRODUCTS, PREFERRED FISH PRODUCTS WITH LONG HALLABILITY |
| SE428412B (en) * | 1982-03-31 | 1983-07-04 | Alfa Laval Ab | PROCEDURE FOR DIVISION OF FRAME AND SKIN MILK |
| SE451791B (en) * | 1984-09-11 | 1987-11-02 | Alfa Laval Food & Dairy Eng | SET AND PLANT FOR PREPARING MILK WITH LOW BACTERIA CONTENT |
| SE8603420L (en) * | 1986-08-14 | 1988-02-15 | Tetra Pak Ab | WANT TO REDUCE HEALTH RISKS IN HANDLING OF PACKAGED, NON-STERILIZED FOOD |
| US4853246A (en) * | 1987-12-01 | 1989-08-01 | Tetra Pak Inc. | Sweetened high protein milk product and process for producing same |
| US5256437A (en) * | 1992-06-19 | 1993-10-26 | Pall Corporation | Product and process of making sterile milk through dynamic microfiltration |
| DK169510B1 (en) * | 1993-05-13 | 1994-11-14 | Apv Pasilac As | Plant and method of treating milk |
-
1995
- 1995-05-17 SE SE9501822A patent/SE506683C2/en not_active IP Right Cessation
- 1995-07-17 UA UA97115511A patent/UA52601C2/en unknown
- 1995-07-17 RU RU97120763A patent/RU2143814C1/en active
- 1995-07-17 DK DK95930747T patent/DK0828429T3/en active
- 1995-07-17 PT PT95930747T patent/PT828429E/en unknown
- 1995-07-17 WO PCT/SE1995/000864 patent/WO1996036238A1/en not_active Ceased
- 1995-07-17 ES ES95930747T patent/ES2186728T3/en not_active Expired - Lifetime
- 1995-07-17 PL PL95323346A patent/PL323346A1/en unknown
- 1995-07-17 AT AT95930747T patent/ATE226020T1/en not_active IP Right Cessation
- 1995-07-17 EE EE9700300A patent/EE03300B1/en not_active IP Right Cessation
- 1995-07-17 EP EP95930747A patent/EP0828429B1/en not_active Expired - Lifetime
- 1995-07-17 HU HU9801662A patent/HU224133B1/en not_active IP Right Cessation
- 1995-07-17 CN CN95197912A patent/CN1061516C/en not_active Expired - Lifetime
- 1995-07-17 SI SI9520155A patent/SI9520155A/en not_active IP Right Cessation
- 1995-07-17 NZ NZ292283A patent/NZ292283A/en not_active IP Right Cessation
- 1995-07-17 BR BR9510588A patent/BR9510588A/en not_active Application Discontinuation
- 1995-07-17 CA CA002221164A patent/CA2221164C/en not_active Expired - Lifetime
- 1995-07-17 AU AU34012/95A patent/AU701569B2/en not_active Expired
- 1995-07-17 KR KR1019970708144A patent/KR100384657B1/en not_active Expired - Lifetime
- 1995-07-17 MX MX9708723A patent/MX9708723A/en unknown
- 1995-07-17 US US08/945,859 patent/US5935632A/en not_active Expired - Lifetime
- 1995-07-17 JP JP53473496A patent/JP3667343B2/en not_active Expired - Lifetime
- 1995-07-17 DE DE69528605T patent/DE69528605T2/en not_active Expired - Lifetime
- 1995-07-17 CZ CZ19973632A patent/CZ291739B6/en not_active IP Right Cessation
-
1997
- 1997-11-14 FI FI974246A patent/FI119904B/en not_active IP Right Cessation
- 1997-11-14 LV LVP-97-231A patent/LV11978B/en unknown
- 1997-11-24 LT LT97-181A patent/LT4376B/en not_active IP Right Cessation
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